WO2021217474A1 - Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace - Google Patents

Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace Download PDF

Info

Publication number
WO2021217474A1
WO2021217474A1 PCT/CN2020/087699 CN2020087699W WO2021217474A1 WO 2021217474 A1 WO2021217474 A1 WO 2021217474A1 CN 2020087699 W CN2020087699 W CN 2020087699W WO 2021217474 A1 WO2021217474 A1 WO 2021217474A1
Authority
WO
WIPO (PCT)
Prior art keywords
reverse
pipe
air outlet
material box
gas
Prior art date
Application number
PCT/CN2020/087699
Other languages
French (fr)
Chinese (zh)
Inventor
刘鹏
徐文立
胡芳
Original Assignee
宁波恒普真空技术有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 宁波恒普真空技术有限公司 filed Critical 宁波恒普真空技术有限公司
Priority to PCT/CN2020/087699 priority Critical patent/WO2021217474A1/en
Priority to CN202080004093.9A priority patent/CN112512728B/en
Priority to JP2022600055U priority patent/JP3241481U/en
Publication of WO2021217474A1 publication Critical patent/WO2021217474A1/en

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/10Sintering only
    • B22F3/1003Use of special medium during sintering, e.g. sintering aid
    • B22F3/1007Atmosphere
    • B22F3/101Changing atmosphere
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Definitions

  • the invention relates to the technical field of a sintering process and a sintering furnace, in particular to a two-way atmosphere control process and a two-way atmosphere sintering furnace.
  • Powder metallurgy products such as MIM are used in various fields, such as consumer electronics, medical equipment, auto parts, smart wear, hardware tools, optical fiber communications, military supplies, etc., which require high product size and performance.
  • the yield rate of full furnace products is low, especially for products that are difficult to burn.
  • the yield rate of products sintered from the same furnace is further improved.
  • the sintering furnace in the prior art mainly has the following air intake methods: 1. The gas is directly filled into the material box; 2. The gas outside the material box is fed by the air inlet valve; 3. The upper and lower safety valves are aired; 4. Intake from the side plate to shorten the air flow stroke.
  • the above types of sintering furnaces only have a one-way air inlet structure, and the gas in the sintering furnace flows in one direction.
  • the furnace body is provided with fixed air inlet and outlet positions.
  • the air inlet is air inlet and the air outlet is air outlet, so that the airflow forms a certain directional flow direction. Because the airflow forms a directional flow direction, the size and performance of the regional products in the flow direction will be different. The main reasons are the following three points:
  • the gas contains impurities such as moisture.
  • impurities such as moisture.
  • the moisture and other impurities in the gas will react with the product, which will affect the product. The impact will become smaller and smaller, and there will be differences before and after the product.
  • the influence of gas flow, velocity and flow status The flow rate and flow rate of the gas flowing through the product near the air inlet position are greater than the flow rate and flow rate of the gas flowing through the product near the air outlet position, and the greater the distance, the more obvious.
  • the airflow passes between the material plate and the material plate. After the airflow passes through a straight line, turbulence will appear. The more the airflow will wash out the product, the smaller the degree of erosion of the product, showing regional product differences.
  • the air outlet plays a throttling effect, and the carbon potential distribution of the product near the air outlet is often obvious (more carbon content).
  • the purpose of the present invention is to provide a two-way atmosphere control process and a two-way atmosphere sintering furnace to solve the technical problem of large differences in product size and performance caused by the use of one-way atmosphere control in the prior art.
  • the present invention provides the following solutions:
  • the invention discloses a two-way atmosphere control process, which includes a preliminary process, a sintering process and a later process.
  • the sintering process includes the following steps:
  • Step A Fill the material box with process gas to form a positive flow of gas
  • Step B Fill the material box with process gas to form a reverse flow of gas.
  • the sintering process further includes the following steps:
  • Step C A vacuum in the material box to form a positive flow of gas
  • Step C B Vacuum in the material box to form a reverse flow of gas.
  • the invention also discloses a two-way atmosphere sintering furnace, which has a forward atmosphere control structure.
  • the forward atmosphere control structure includes a forward air inlet structure and a forward air outlet structure.
  • the gas flows into the material box from the forward air inlet structure. And it flows out of the material box from the forward air outlet structure to form a forward flow of gas, and also has a reverse atmosphere control structure.
  • the reverse atmosphere control structure has a reverse air inlet structure and a reverse air outlet structure, and the gas flows in from the reverse air inlet structure. And it flows out from the reverse air outlet structure to form a reverse flow of gas.
  • the forward air intake structure is a forward air intake pipe, one end of the forward air intake pipe is located outside the sintering furnace, and the other end of the forward air intake pipe is in communication with the material box in the sintering furnace.
  • the forward air outlet structure is a forward air outlet pipe, one end of the forward air outlet pipe is located outside the sintering furnace, and the other end of the forward air outlet pipe is in communication with the material box in the sintering furnace;
  • the reverse air inlet structure is a reverse air inlet pipe
  • the reverse air inlet pipe is a branch pipe of the forward air outlet pipe
  • the reverse air outlet structure is a reverse air outlet pipe
  • the reverse air outlet pipe is a branch pipe of the forward air inlet pipe .
  • the forward air inlet structure is an air inlet valve
  • the air inlet valve is fixed on the material box
  • the forward air outlet structure is a forward air outlet pipe
  • one end of the forward air outlet pipe is located outside the sintering furnace
  • the other end of the forward gas outlet pipe is in communication with the material box in the sintering furnace;
  • the reverse air intake structure is a reverse air intake pipe
  • the reverse air intake pipe is a branch pipe of the forward air outlet pipe
  • the reverse air outlet structure is a splicing gap and a door panel gap on the material box.
  • the positive air intake structure is a safety valve, a splicing gap on the material box, and a door panel gap on the material box, the safety valve is fixed on the material box, and the positive air outlet structure is a positive air outlet pipe, One end of the forward air outlet pipe is located outside the sintering furnace, and the other end of the forward air outlet pipe is in communication with the material box in the sintering furnace;
  • the reverse air intake structure is a reverse air intake pipe
  • the reverse air intake pipe is a branch pipe of the forward air outlet pipe
  • the reverse air outlet structure is a splicing gap and a door panel gap on the material box.
  • the forward air intake structure is an opening on the side plate of the material box
  • the forward air outlet structure is a forward air outlet pipe
  • one end of the forward air outlet pipe is located outside the sintering furnace
  • the forward air outlet pipe The other end of the sintering furnace is connected with the material box in the sintering furnace;
  • the reverse air intake structure is a reverse air intake pipe
  • the reverse air intake pipe is a branch pipe of the forward air outlet pipe
  • the reverse air outlet structure is an opening on a side plate of the material box.
  • the present invention allows the difference in the product size and performance of each region in the flow direction in the one-way atmosphere control to be supplemented by the opposite direction atmosphere control, so that the size and performance of the product are uniform before and after.
  • Figure 1 is a temperature process curve of a sintered product using the bidirectional atmosphere control process of this embodiment
  • Figure 2 is a comparison diagram of the carbon potential distribution curves of products with one-way atmosphere control and two-way atmosphere control after sintering;
  • FIG. 3 is a schematic diagram of a structure of the two-way atmosphere sintering furnace of this embodiment
  • FIG. 4 is a schematic diagram of another structure of the two-way atmosphere sintering furnace of this embodiment.
  • FIG. 5 is a schematic diagram of another structure of the two-way atmosphere sintering furnace of this embodiment.
  • FIG. 6 is a schematic diagram of another structure of the two-way atmosphere sintering furnace of this embodiment.
  • the purpose of the present invention is to provide a two-way atmosphere control process and a two-way atmosphere sintering furnace to solve the technical problem of large differences in product size and performance caused by the use of one-way atmosphere control in the prior art.
  • This embodiment provides a two-way atmosphere control process, which includes a pre-process GI, a sintering process GII, and a post-process GIII.
  • the sintering process is more complicated. This embodiment only describes the content related to the gas flow, and the other content of the sintering process can refer to the prior art.
  • the sintering process GII includes the following steps:
  • Step A Fill the material box 2 with process gas to form a positive gas flow
  • Step B Fill the material box 2 with process gas to form a reverse flow of gas.
  • the reverse-direction atmosphere control is added, so that products with insufficient atmosphere in the previous one-way atmosphere control process can be supplemented, especially products with serious deviations in size and carbon content near the original gas outlet level.
  • Has played a very good effect the whole furnace product is sintered, and the size is very uniform.
  • the original one-way atmosphere control is defined as the forward atmosphere control
  • the reverse atmosphere control is defined as the reverse atmosphere control.
  • the process of vacuuming the material box 2 in the vacuum sintering process also involves the flow of gas. Therefore, in order to further improve the uniformity of the size and performance of the product, the sintering process of this embodiment further includes the following steps:
  • Step C A vacuum inside the material box 2 to form a positive flow of gas
  • Step C B vacuum in the material box 2 to form a reverse flow of gas.
  • the step A can be made, Step B continuously, so that steps C A, C B continuously Step; Step C A can be inserted and / or Step C B between step A and step B.
  • the present embodiment referred to as the forward flow and reverse flow opposite to the flow direction, the same as in Step C A gas stream of step A in the direction of the present embodiment, the same gas flow direction in the step B and step C B of the present embodiment .
  • the pre-process G I is mainly a basic process under the premise of heating, such as a degreasing process (if there is no degreasing process, it can be directly heated and kept warm to prepare for direct sintering of the product).
  • the temperature range of the preliminary step GI is from room temperature to 700°C, and preferably from room temperature to 600°C.
  • the latter process GIII is mainly the basic process under the premise of cooling, and it is immediately after the end of the sintering process GII, such as the cooling process.
  • the temperature range of the post-process GIII is: the temperature is lowered from 1400°C, preferably from 1200°C.
  • the temperature range during the sintering process GII is 600° C. to 1600° C., preferably 600° C. to 1400° C., including a heating stage, a holding stage and a cooling stage, and the heating stage includes a linear heating and a stepped heating.
  • the furnace is charged with process gas or nitrogen or argon or a mixture of hydrogen gas
  • the step A, step B, and the pressure and flow rate within the inflatable Step C A and C B in the hopper Step 2 embodiment can be kept constant
  • the value may also be a variable value, which can be selected by those skilled in the art according to actual needs.
  • the pressure value in the furnace of Step A and Step B is 0.01 Pa to 1000 KPa, preferably 1 KPa to 100 KPa.
  • the inflation flow value of step A and step B is 1L/min-500L/min, preferably 1L-200L/min.
  • Figure 1 is a temperature process curve of MIM products in a sintering furnace.
  • A1, A2, and A3 are the first, second, and third forward inflation respectively, and so on; B1, B2, B3 They are the first, second, third reverse inflation, and so on.
  • Figure 2 is a comparison diagram of the carbon potential distribution curves of MIM products after sintering in a unidirectional atmosphere and a bidirectional atmosphere. It can be seen that the bidirectional atmosphere control greatly improves the carbon content distribution deviation problem compared to the unidirectional atmosphere control.
  • This embodiment also provides a two-way atmosphere sintering furnace, which has a forward atmosphere control structure (or one-way atmosphere control structure) commonly used in existing sintering furnaces.
  • the forward atmosphere control structure includes a forward air inlet structure and a forward air outlet structure. Structure, the gas flows into the material box 2 from the positive air inlet structure and flows out of the material box 2 from the positive air outlet structure, forming a positive flow of gas.
  • This embodiment adds a reverse atmosphere control structure on the basis of the prior art.
  • the reverse atmosphere control structure has a reverse air intake structure and a reverse air output structure. Gas flows in from the reverse air intake structure and flows out from the reverse air output structure to form a reverse gas flow. .
  • the reverse airflow control structure can have many forms, as long as it can form a reverse airflow opposite to the forward airflow.
  • the following is an example of the reverse atmosphere control structure for four common sintering furnace structures. But it is not limited to the following four layout forms.
  • the reverse air inlet pipe 5 is a branch of the forward air outlet pipe 4, but those skilled in the art can also make one end of the reverse air inlet pipe 5 located outside the sintering furnace, and the other end of the reverse air inlet pipe 5 is connected to the sintering furnace.
  • the inner tank 2 is connected, and the reverse air inlet pipe 5 is arranged adjacent to the forward air outlet pipe 4, so that the outlet of the forward airflow is very close to the inlet of the reverse airflow, and the two-way atmosphere control can also be realized.
  • the forward air intake structure is a forward air intake pipe 3.
  • One end of the forward air intake pipe 3 is located outside the furnace body 1 of the sintering furnace, and the other end of the forward air intake pipe 3 is connected with the material box 2 in the sintering furnace.
  • the forward air outlet structure is a forward air outlet pipe 4, one end of the forward air outlet pipe 4 is located outside the furnace body 1 of the sintering furnace, and the other end of the forward air outlet pipe 4 is connected with the material box 2 in the sintering furnace;
  • the reverse air inlet structure is a reverse air inlet pipe 5, the reverse air inlet pipe 5 is a branch pipe of the forward air outlet pipe 4, the reverse air outlet structure is a reverse air outlet pipe 6, and the reverse air outlet pipe 6 is a branch pipe of the forward air inlet pipe 3.
  • FIG. 4 it is a sintering furnace structure in which gas enters the material box 2 through the air inlet valve 7 on the material box 2.
  • the positive air intake structure is an air intake valve 7, which is fixed on the material box 2
  • the forward air output structure is a forward air outlet pipe 4, and one end of the forward air outlet pipe 4 is located in the furnace body of the sintering furnace. 1. Outside, the other end of the forward gas outlet pipe 4 is connected with the material box 2 in the sintering furnace;
  • the reverse air inlet structure is a reverse air inlet pipe 5, the reverse air inlet pipe 5 is a branch pipe of the forward air outlet pipe 4, and the reverse air outlet structure is a splicing gap on the material box 2 and a door panel gap.
  • FIG. 5 it is a sintering furnace structure in which gas enters the material box 2 through the safety valve 8 on the material box 2 and the gap on the material box 2.
  • the positive air intake structure is the safety valve 8, the splicing gap on the material box 2, and the door panel gap on the material box 2.
  • the safety valve 8 is fixed on the material box 2, and the positive air outlet structure is the positive air outlet pipe 4.
  • One end of the forward air outlet pipe 4 is located outside the furnace body 1 of the sintering furnace, and the other end of the forward air outlet pipe 4 is connected with the material box 2 in the sintering furnace;
  • the reverse air inlet structure is a reverse air inlet pipe 5, the reverse air inlet pipe 5 is a branch pipe of the forward air outlet pipe 4, and the reverse air outlet structure is a splicing gap on the material box 2 and a door panel gap.
  • FIG. 6 it is a sintering furnace structure in which gas enters the material box 2 through the opening on the side plate of the material box 2.
  • the forward air intake structure is an opening on the side plate of the material box 2
  • the forward air output structure is a forward air outlet pipe 4.
  • One end of the forward air outlet pipe 4 is located outside the furnace body 1 of the sintering furnace, and the forward air outlet pipe The other end of 4 is connected with the material box 2 in the sintering furnace;
  • the reverse air intake structure is a reverse air intake pipe 5, the reverse air intake pipe 5 is a branch pipe of the forward air outlet pipe 4, and the reverse air outlet structure is an opening on the side plate of the material box 2.
  • Table 1 shows the product size distribution and CPK obtained under one-way atmosphere control
  • Table 2 shows the product size distribution and CPK obtained under two-way atmosphere control.
  • Standard deviation refers to the uniformity of fluctuations in all dimensions, and the smaller the value, the better.
  • CPK refers to a measure of production feasibility, the benchmark value is 1.33, the larger the value, the better. The comparison shows that the use of the two-way atmosphere control process effectively improves the shortcomings of the one-way atmosphere control process.

Abstract

Disclosed are a bidirectional atmosphere control process and a bidirectional atmosphere sintering furnace. The invention employs bidirectional atmosphere control, such that differences in size and performance of products in respective regions arising from unidirectional atmosphere control can be compensated for by atmosphere control performed in an opposite direction, thereby enabling products placed in the front and back of a furnace to have uniform size and performance.

Description

一种双向气氛控制工艺及双向气氛烧结炉Two-way atmosphere control process and two-way atmosphere sintering furnace 技术领域Technical field
本发明涉及烧结工艺及烧结炉技术领域,特别是涉及一种双向气氛控制工艺及双向气氛烧结炉。The invention relates to the technical field of a sintering process and a sintering furnace, in particular to a two-way atmosphere control process and a two-way atmosphere sintering furnace.
背景技术Background technique
MIM等粉末冶金产品应用于各领域,如消费类电子、医疗器械、汽车零部件、智能穿戴、五金工具、光纤通讯、军工用品等,对产品尺寸和性能的要求较高。但是满炉产品良率低,特别是难烧的产品,同炉产品烧结出来的尺寸和性能存在差异性,产品出炉良率有待进一步提高。Powder metallurgy products such as MIM are used in various fields, such as consumer electronics, medical equipment, auto parts, smart wear, hardware tools, optical fiber communications, military supplies, etc., which require high product size and performance. However, the yield rate of full furnace products is low, especially for products that are difficult to burn. There are differences in the size and performance of products sintered from the same furnace, and the yield rate of products needs to be further improved.
现有技术中的烧结炉主要有以下几种进气方式:1.料箱内直接充入气体;2.料箱外的气体由进气阀进气;3.上、下安全阀进气;4.由侧板处进气,减短气流行程。以上几种烧结炉均只具备单向进气结构,烧结炉内气体为单向流动。其炉体上设有固定的进气位与出气位,在脱脂与烧结过程中,进气位进气,出气位出气,使气流形成一定定向流向。由于气流形成定向流向,会造成流动方向上区域产品的尺寸与性能的差异性,主要原因有以下三点:The sintering furnace in the prior art mainly has the following air intake methods: 1. The gas is directly filled into the material box; 2. The gas outside the material box is fed by the air inlet valve; 3. The upper and lower safety valves are aired; 4. Intake from the side plate to shorten the air flow stroke. The above types of sintering furnaces only have a one-way air inlet structure, and the gas in the sintering furnace flows in one direction. The furnace body is provided with fixed air inlet and outlet positions. During the degreasing and sintering process, the air inlet is air inlet and the air outlet is air outlet, so that the airflow forms a certain directional flow direction. Because the airflow forms a directional flow direction, the size and performance of the regional products in the flow direction will be different. The main reasons are the following three points:
1.气体中成份(杂质)的影响。气体中含有水份等杂质,当气流经过产品,气体中的水份等杂质会与产品反应,使产品受影响,气流中的杂质在前面反应掉了,到后面流经产品的气流对产品的影响会越来越小,出现产品前后差异性。1. The influence of components (impurities) in the gas. The gas contains impurities such as moisture. When the gas flow passes through the product, the moisture and other impurities in the gas will react with the product, which will affect the product. The impact will become smaller and smaller, and there will be differences before and after the product.
2.产品中挥发物的影响。比如在前期脱脂工序中,在受热过程中,产品中的粘结剂会从产品中挥发出来,然后随着气流方向进入出气口,这就会形成前面产品中跑出的挥发物跑到后面去,粘附在后面的产品表面上,形成前后产品差异性。2. The influence of volatile matter in the product. For example, in the pre-degreasing process, during the heating process, the adhesive in the product will volatilize from the product, and then enter the air outlet along the direction of the airflow, which will form the volatiles from the previous product and run to the back. , Adhere to the surface of the back product, forming the difference between the front and back products.
3.气体的流量、流速及流动状态的影响。在靠近进气位置的产品流经的气体的流量与流速比靠近出气口位置的产品流经的气体的流量与流速要大,且距离越大越明显。气流经过料板与料板之间,气流经过一段直线 后会出现乱流现象,越到最后气流对产品的冲刷程度就越小,呈现区域产品性差异。再加上出气口起到节流作用,往往在出气口附近的产品碳势分布明显(含碳量较多)。3. The influence of gas flow, velocity and flow status. The flow rate and flow rate of the gas flowing through the product near the air inlet position are greater than the flow rate and flow rate of the gas flowing through the product near the air outlet position, and the greater the distance, the more obvious. The airflow passes between the material plate and the material plate. After the airflow passes through a straight line, turbulence will appear. The more the airflow will wash out the product, the smaller the degree of erosion of the product, showing regional product differences. In addition, the air outlet plays a throttling effect, and the carbon potential distribution of the product near the air outlet is often obvious (more carbon content).
发明内容Summary of the invention
本发明的目的是提供一种双向气氛控制工艺及双向气氛烧结炉,用以解决现有技术中采用单向气氛控制导致的产品尺寸与性能的差异性较大的技术问题。The purpose of the present invention is to provide a two-way atmosphere control process and a two-way atmosphere sintering furnace to solve the technical problem of large differences in product size and performance caused by the use of one-way atmosphere control in the prior art.
为实现上述目的,本发明提供了如下方案:In order to achieve the above objectives, the present invention provides the following solutions:
本发明公开了一种双向气氛控制工艺,包括前期工序、烧结工序和后期工序,烧结工序中包括以下步骤:The invention discloses a two-way atmosphere control process, which includes a preliminary process, a sintering process and a later process. The sintering process includes the following steps:
步骤A、向料箱内充入工艺气体,形成气体正向流动;Step A: Fill the material box with process gas to form a positive flow of gas;
步骤B、向料箱内充入工艺气体,形成气体逆向流动。Step B: Fill the material box with process gas to form a reverse flow of gas.
优选地,烧结工序中还包括以下步骤:Preferably, the sintering process further includes the following steps:
步骤C A、在料箱内抽真空,形成气体正向流动; Step C A , vacuum in the material box to form a positive flow of gas;
步骤C B、在料箱内抽真空,形成气体逆向流动。 Step C B. Vacuum in the material box to form a reverse flow of gas.
本发明还公开了一种双向气氛烧结炉,具有正向气氛控制结构,所述正向气氛控制结构包括正向进气结构和正向出气结构,气体由所述正向进气结构流入料箱内并由所述正向出气结构流出料箱,形成气体正向流动,还具有逆向气氛控制结构,所述逆向气氛控制结构具有逆向进气结构和逆向出气结构,气体由所述逆向进气结构流入并由所述逆向出气结构流出,形成气体逆向流动。The invention also discloses a two-way atmosphere sintering furnace, which has a forward atmosphere control structure. The forward atmosphere control structure includes a forward air inlet structure and a forward air outlet structure. The gas flows into the material box from the forward air inlet structure. And it flows out of the material box from the forward air outlet structure to form a forward flow of gas, and also has a reverse atmosphere control structure. The reverse atmosphere control structure has a reverse air inlet structure and a reverse air outlet structure, and the gas flows in from the reverse air inlet structure. And it flows out from the reverse air outlet structure to form a reverse flow of gas.
优选地,所述正向进气结构为正向进气管,所述正向进气管的一端位于烧结炉外,所述正向进气管的另一端与烧结炉内的料箱连通,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;Preferably, the forward air intake structure is a forward air intake pipe, one end of the forward air intake pipe is located outside the sintering furnace, and the other end of the forward air intake pipe is in communication with the material box in the sintering furnace. The forward air outlet structure is a forward air outlet pipe, one end of the forward air outlet pipe is located outside the sintering furnace, and the other end of the forward air outlet pipe is in communication with the material box in the sintering furnace;
所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,所述逆向出气结构为逆向出气管,所述逆向出气管为所述正向进气管的支管。The reverse air inlet structure is a reverse air inlet pipe, the reverse air inlet pipe is a branch pipe of the forward air outlet pipe, the reverse air outlet structure is a reverse air outlet pipe, and the reverse air outlet pipe is a branch pipe of the forward air inlet pipe .
优选地,所述正向进气结构为进气阀,所述进气阀固定于料箱上,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;Preferably, the forward air inlet structure is an air inlet valve, the air inlet valve is fixed on the material box, the forward air outlet structure is a forward air outlet pipe, and one end of the forward air outlet pipe is located outside the sintering furnace , The other end of the forward gas outlet pipe is in communication with the material box in the sintering furnace;
所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,所述逆向出气结构为料箱上的拼接缝隙和门板缝隙。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, and the reverse air outlet structure is a splicing gap and a door panel gap on the material box.
优选地,所述正向进气结构为安全阀、料箱上的拼接缝隙、料箱上的门板缝隙,所述安全阀固定于料箱上,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;Preferably, the positive air intake structure is a safety valve, a splicing gap on the material box, and a door panel gap on the material box, the safety valve is fixed on the material box, and the positive air outlet structure is a positive air outlet pipe, One end of the forward air outlet pipe is located outside the sintering furnace, and the other end of the forward air outlet pipe is in communication with the material box in the sintering furnace;
所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,所述逆向出气结构为料箱上的拼接缝隙和门板缝隙。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, and the reverse air outlet structure is a splicing gap and a door panel gap on the material box.
优选地,所述正向进气结构为料箱侧板上的开口,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;Preferably, the forward air intake structure is an opening on the side plate of the material box, the forward air outlet structure is a forward air outlet pipe, one end of the forward air outlet pipe is located outside the sintering furnace, and the forward air outlet pipe The other end of the sintering furnace is connected with the material box in the sintering furnace;
所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,所述逆向出气结构为料箱侧板上的开口。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, and the reverse air outlet structure is an opening on a side plate of the material box.
本发明相对于现有技术取得了以下技术效果:Compared with the prior art, the present invention has achieved the following technical effects:
本发明通过双向气氛控制,让单向气氛控制中流动方向上各区域产品尺寸、性能出现的差异得到反方向气氛控制的补足,使产品的尺寸、性能前后均匀。Through the two-way atmosphere control, the present invention allows the difference in the product size and performance of each region in the flow direction in the one-way atmosphere control to be supplemented by the opposite direction atmosphere control, so that the size and performance of the product are uniform before and after.
附图说明Description of the drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the following will briefly introduce the drawings that need to be used in the embodiments. Obviously, the drawings in the following description are only some of the present invention. Embodiments, for those of ordinary skill in the art, without creative work, other drawings can be obtained based on these drawings.
图1为使用本实施例的双向气氛控制工艺烧结产品的温度工艺曲线;Figure 1 is a temperature process curve of a sintered product using the bidirectional atmosphere control process of this embodiment;
图2为单向气氛控制和双向气氛控制的产品在烧结后的碳势分布曲线对比图;Figure 2 is a comparison diagram of the carbon potential distribution curves of products with one-way atmosphere control and two-way atmosphere control after sintering;
图3为本实施例双向气氛烧结炉的一种结构示意图;FIG. 3 is a schematic diagram of a structure of the two-way atmosphere sintering furnace of this embodiment;
图4为本实施例双向气氛烧结炉的又一种结构示意图;4 is a schematic diagram of another structure of the two-way atmosphere sintering furnace of this embodiment;
图5为本实施例双向气氛烧结炉的又一种结构示意图;FIG. 5 is a schematic diagram of another structure of the two-way atmosphere sintering furnace of this embodiment;
图6为本实施例双向气氛烧结炉的又一种结构示意图;6 is a schematic diagram of another structure of the two-way atmosphere sintering furnace of this embodiment;
附图标记说明:1炉体;2料箱;3正向进气管;4正向出气管;5逆向进气管;6逆向出气管;7进气阀;8安全阀。Description of reference signs: 1 furnace body; 2 material box; 3 forward air inlet pipe; 4 forward air outlet pipe; 5 reverse air inlet pipe; 6 reverse air outlet pipe; 7 air inlet valve; 8 safety valve.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work shall fall within the protection scope of the present invention.
本发明的目的是提供一种双向气氛控制工艺及双向气氛烧结炉,用以解决现有技术中采用单向气氛控制导致的产品尺寸与性能的差异性较大的技术问题。The purpose of the present invention is to provide a two-way atmosphere control process and a two-way atmosphere sintering furnace to solve the technical problem of large differences in product size and performance caused by the use of one-way atmosphere control in the prior art.
为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合附图和具体实施方式对本发明作进一步详细的说明。In order to make the above-mentioned objects, features and advantages of the present invention more obvious and understandable, the present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.
本实施例提供一种双向气氛控制工艺,包括前期工序GⅠ、烧结工序GⅡ和后期工序GⅢ。烧结工序较为复杂,本实施例仅对涉及气体流动的内容进行说明,烧结工序的其它内容参照现有技术即可。烧结工序GⅡ中包括以下步骤:This embodiment provides a two-way atmosphere control process, which includes a pre-process GI, a sintering process GII, and a post-process GIII. The sintering process is more complicated. This embodiment only describes the content related to the gas flow, and the other content of the sintering process can refer to the prior art. The sintering process GII includes the following steps:
步骤A、向料箱2内充入工艺气体,形成气体正向流动;Step A: Fill the material box 2 with process gas to form a positive gas flow;
步骤B、向料箱2内充入工艺气体,形成气体逆向流动。Step B: Fill the material box 2 with process gas to form a reverse flow of gas.
本实施例在现有技术采用单向气氛控制的基础上增加反方向气氛控制,使之前单向气氛控制工艺气氛不足的产品得到补足,特别是靠近原出气位附近尺寸及碳含量偏差严重的产品,起到了非常好的效果,整炉产品烧结下来,尺寸非常均匀。将原单向气氛控制定义为顺向气氛控制,反方向气氛控制定义为逆向气氛控制。In this embodiment, on the basis of the one-way atmosphere control in the prior art, the reverse-direction atmosphere control is added, so that products with insufficient atmosphere in the previous one-way atmosphere control process can be supplemented, especially products with serious deviations in size and carbon content near the original gas outlet level. , Has played a very good effect, the whole furnace product is sintered, and the size is very uniform. The original one-way atmosphere control is defined as the forward atmosphere control, and the reverse atmosphere control is defined as the reverse atmosphere control.
除了向料箱2内充入气体的过程涉及气体的流动外,真空烧结工艺中对料箱2抽真空的过程也涉及气体的流动。因此,为了进一步改善产品的尺寸与性能的均匀性,本实施例的烧结工序中还包括以下步骤:In addition to the process of filling the material box 2 with gas, the process of vacuuming the material box 2 in the vacuum sintering process also involves the flow of gas. Therefore, in order to further improve the uniformity of the size and performance of the product, the sintering process of this embodiment further includes the following steps:
步骤C A、在料箱2内抽真空,形成气体正向流动; Step C A , vacuum inside the material box 2 to form a positive flow of gas;
步骤C B、在料箱2内抽真空,形成气体逆向流动。 Step C B , vacuum in the material box 2 to form a reverse flow of gas.
在具体实施时,可以使步骤A、步骤B连续进行,使步骤C A、步骤C B连续进行;也可以在步骤A与步骤B之间插入步骤C A和/或步骤C B。需要说明的是,本实施例所指正向流动和逆向流动为相反的流动方向,本实施例中步骤C A与步骤A的气流方向相同,本实施例中步骤C B与步骤B的气流方向相同。 In a specific embodiment, the step A can be made, Step B continuously, so that steps C A, C B continuously Step; Step C A can be inserted and / or Step C B between step A and step B. Incidentally, the present embodiment referred to as the forward flow and reverse flow opposite to the flow direction, the same as in Step C A gas stream of step A in the direction of the present embodiment, the same gas flow direction in the step B and step C B of the present embodiment .
具体的,前期工序GⅠ主要为升温前提下的基础工艺,如脱脂工艺(如果无脱脂工艺,可以是直接升温并保温,为产品直接烧结作预备)。前期工序GⅠ的温度区间为室温~700℃,并优选为室温~600℃。后期工序GⅢ主要为降温前提下的基础工艺,紧接在烧结工序GⅡ结束,如冷却工艺。后期工序GⅢ的温度区间为:从1400℃开始降温,优选为从1200℃开始降温。烧结工序GⅡ期间的温度范围为600℃~1600℃,优选为600℃~1400℃,包括升温阶段与保温阶段及降温阶段,升温阶段包括直线升温和阶梯升温。Specifically, the pre-process G I is mainly a basic process under the premise of heating, such as a degreasing process (if there is no degreasing process, it can be directly heated and kept warm to prepare for direct sintering of the product). The temperature range of the preliminary step GI is from room temperature to 700°C, and preferably from room temperature to 600°C. The latter process GⅢ is mainly the basic process under the premise of cooling, and it is immediately after the end of the sintering process GII, such as the cooling process. The temperature range of the post-process GIII is: the temperature is lowered from 1400°C, preferably from 1200°C. The temperature range during the sintering process GII is 600° C. to 1600° C., preferably 600° C. to 1400° C., including a heating stage, a holding stage and a cooling stage, and the heating stage includes a linear heating and a stepped heating.
本实施例中,炉内充入的工艺气体为氮气或氩气或氢气或混合气,步骤A、步骤B、步骤C A与步骤C B中料箱2内的压力和充气流量,可以保持恒定值,也可以为变动值,本领域技术人员可以根据实际需要进行选择。 Embodiment, the furnace is charged with process gas or nitrogen or argon or a mixture of hydrogen gas, the step A, step B, and the pressure and flow rate within the inflatable Step C A and C B in the hopper Step 2 embodiment, can be kept constant The value may also be a variable value, which can be selected by those skilled in the art according to actual needs.
步骤A和步骤B的炉内压力值为0.01Pa~1000KPa,优选为1KPa~100KPa。The pressure value in the furnace of Step A and Step B is 0.01 Pa to 1000 KPa, preferably 1 KPa to 100 KPa.
步骤A和步骤B的充气流量值为1L/min~500L/min,优选为1L~200L/min。The inflation flow value of step A and step B is 1L/min-500L/min, preferably 1L-200L/min.
图1为MIM产品在烧结炉中的一种温度工艺曲线,图1中A1、A2、A3分别为第一次、第二次、第三次正向充气,依此类推;B1、B2、B3分别为第一次、第二次、第三次逆向充气,依此类推。C1代表一次抽真空过程,包括一次步骤C A与一次步骤C B。图2为MIM产品在单向气氛和双 向气氛烧结后的碳势分布曲线对比图,可以看到,双向气氛控制相比于单向气氛控制,极大地改善了碳含量的分布偏差问题。 Figure 1 is a temperature process curve of MIM products in a sintering furnace. In Figure 1, A1, A2, and A3 are the first, second, and third forward inflation respectively, and so on; B1, B2, B3 They are the first, second, third reverse inflation, and so on. C1 representative of a vacuum process, comprising a first step of Step C A and C B. Figure 2 is a comparison diagram of the carbon potential distribution curves of MIM products after sintering in a unidirectional atmosphere and a bidirectional atmosphere. It can be seen that the bidirectional atmosphere control greatly improves the carbon content distribution deviation problem compared to the unidirectional atmosphere control.
本实施例还提供一种双向气氛烧结炉,其具有现有烧结炉中常用的正向气氛控制结构(或称单向气氛控制结构),正向气氛控制结构包括正向进气结构和正向出气结构,气体由正向进气结构流入料箱2内并由正向出气结构流出料箱2,形成气体正向流动。本实施例在现有技术的基础上,增加了逆向气氛控制结构,逆向气氛控制结构具有逆向进气结构和逆向出气结构,气体由逆向进气结构流入并由逆向出气结构流出,形成气体逆向流动。根据烧结炉类型的不同,逆向逆风控制结构可以有多种形式,只要能形成与正向气流相反的逆向气流即可,下面对四种常见的烧结炉结构进行逆向气氛控制结构的举例说明,但不局限于以下四种布置形式。例如,以下四种结构中逆向进气管5均为正向出气管4的支管,但本领域技术人员也可使逆向进气管5的一端位于烧结炉外,逆向进气管5的另一端与烧结炉内的料箱2连通,并使逆向进气管5与正向出气管4相邻设置,这样,正向气流的出口和逆向气流的进口极为接近,同样也可实现双向气氛控制。This embodiment also provides a two-way atmosphere sintering furnace, which has a forward atmosphere control structure (or one-way atmosphere control structure) commonly used in existing sintering furnaces. The forward atmosphere control structure includes a forward air inlet structure and a forward air outlet structure. Structure, the gas flows into the material box 2 from the positive air inlet structure and flows out of the material box 2 from the positive air outlet structure, forming a positive flow of gas. This embodiment adds a reverse atmosphere control structure on the basis of the prior art. The reverse atmosphere control structure has a reverse air intake structure and a reverse air output structure. Gas flows in from the reverse air intake structure and flows out from the reverse air output structure to form a reverse gas flow. . Depending on the type of sintering furnace, the reverse airflow control structure can have many forms, as long as it can form a reverse airflow opposite to the forward airflow. The following is an example of the reverse atmosphere control structure for four common sintering furnace structures. But it is not limited to the following four layout forms. For example, in the following four structures, the reverse air inlet pipe 5 is a branch of the forward air outlet pipe 4, but those skilled in the art can also make one end of the reverse air inlet pipe 5 located outside the sintering furnace, and the other end of the reverse air inlet pipe 5 is connected to the sintering furnace. The inner tank 2 is connected, and the reverse air inlet pipe 5 is arranged adjacent to the forward air outlet pipe 4, so that the outlet of the forward airflow is very close to the inlet of the reverse airflow, and the two-way atmosphere control can also be realized.
如图3所示,其为料箱2(或称马弗)内直接充入气体的烧结炉结构。图3中,正向进气结构为正向进气管3,正向进气管3的一端位于烧结炉的炉体1外,正向进气管3的另一端与烧结炉内的料箱2连通,正向出气结构为正向出气管4,正向出气管4的一端位于烧结炉的炉体1外,正向出气管4的另一端与烧结炉内的料箱2连通;As shown in Fig. 3, it is a sintering furnace structure in which the material box 2 (or muffle) is directly filled with gas. In Fig. 3, the forward air intake structure is a forward air intake pipe 3. One end of the forward air intake pipe 3 is located outside the furnace body 1 of the sintering furnace, and the other end of the forward air intake pipe 3 is connected with the material box 2 in the sintering furnace. The forward air outlet structure is a forward air outlet pipe 4, one end of the forward air outlet pipe 4 is located outside the furnace body 1 of the sintering furnace, and the other end of the forward air outlet pipe 4 is connected with the material box 2 in the sintering furnace;
逆向进气结构为逆向进气管5,逆向进气管5为正向出气管4的支管,逆向出气结构为逆向出气管6,逆向出气管6为正向进气管3的支管。The reverse air inlet structure is a reverse air inlet pipe 5, the reverse air inlet pipe 5 is a branch pipe of the forward air outlet pipe 4, the reverse air outlet structure is a reverse air outlet pipe 6, and the reverse air outlet pipe 6 is a branch pipe of the forward air inlet pipe 3.
如图4所示,其为气体由料箱2上的进气阀7进入料箱2的烧结炉结构。图4中,正向进气结构为进气阀7,进气阀7固定于料箱2上,正向出气结构为正向出气管4,正向出气管4的一端位于烧结炉的炉体1外,正向出气管4的另一端与烧结炉内的料箱2连通;As shown in FIG. 4, it is a sintering furnace structure in which gas enters the material box 2 through the air inlet valve 7 on the material box 2. In Figure 4, the positive air intake structure is an air intake valve 7, which is fixed on the material box 2, and the forward air output structure is a forward air outlet pipe 4, and one end of the forward air outlet pipe 4 is located in the furnace body of the sintering furnace. 1. Outside, the other end of the forward gas outlet pipe 4 is connected with the material box 2 in the sintering furnace;
逆向进气结构为逆向进气管5,逆向进气管5为正向出气管4的支管,逆向出气结构为料箱2上的拼接缝隙和门板缝隙。The reverse air inlet structure is a reverse air inlet pipe 5, the reverse air inlet pipe 5 is a branch pipe of the forward air outlet pipe 4, and the reverse air outlet structure is a splicing gap on the material box 2 and a door panel gap.
如图5所示,其为气体由料箱2上的安全阀8和料箱2上的缝隙进入料箱2的烧结炉结构。图5中,正向进气结构为安全阀8、料箱2上的拼接缝隙、料箱2上的门板缝隙,安全阀8固定于料箱2上,正向出气结构为正向出气管4,正向出气管4的一端位于烧结炉的炉体1外,正向出气管4的另一端与烧结炉内的料箱2连通;As shown in FIG. 5, it is a sintering furnace structure in which gas enters the material box 2 through the safety valve 8 on the material box 2 and the gap on the material box 2. In Figure 5, the positive air intake structure is the safety valve 8, the splicing gap on the material box 2, and the door panel gap on the material box 2. The safety valve 8 is fixed on the material box 2, and the positive air outlet structure is the positive air outlet pipe 4. , One end of the forward air outlet pipe 4 is located outside the furnace body 1 of the sintering furnace, and the other end of the forward air outlet pipe 4 is connected with the material box 2 in the sintering furnace;
逆向进气结构为逆向进气管5,逆向进气管5为正向出气管4的支管,逆向出气结构为料箱2上的拼接缝隙和门板缝隙。The reverse air inlet structure is a reverse air inlet pipe 5, the reverse air inlet pipe 5 is a branch pipe of the forward air outlet pipe 4, and the reverse air outlet structure is a splicing gap on the material box 2 and a door panel gap.
如图6所示,其为气体由料箱2侧板上的开口进入料箱2的烧结炉结构。图6中,正向进气结构为料箱2侧板上的开口,正向出气结构为正向出气管4,正向出气管4的一端位于烧结炉的炉体1外,正向出气管4的另一端与烧结炉内的料箱2连通;As shown in FIG. 6, it is a sintering furnace structure in which gas enters the material box 2 through the opening on the side plate of the material box 2. In Figure 6, the forward air intake structure is an opening on the side plate of the material box 2, and the forward air output structure is a forward air outlet pipe 4. One end of the forward air outlet pipe 4 is located outside the furnace body 1 of the sintering furnace, and the forward air outlet pipe The other end of 4 is connected with the material box 2 in the sintering furnace;
逆向进气结构为逆向进气管5,逆向进气管5为正向出气管4的支管,逆向出气结构为料箱2侧板上的开口。The reverse air intake structure is a reverse air intake pipe 5, the reverse air intake pipe 5 is a branch pipe of the forward air outlet pipe 4, and the reverse air outlet structure is an opening on the side plate of the material box 2.
以下为使用图5所示烧结炉,用316材料的手柄所烧结的数据。表1为单向气氛控制下得到的产品尺寸分布及CPK,表2为双向气氛控制下得到的产品尺寸分布及CPK。The following is the sintering data using the sintering furnace shown in Figure 5 with a handle made of 316 material. Table 1 shows the product size distribution and CPK obtained under one-way atmosphere control, and Table 2 shows the product size distribution and CPK obtained under two-way atmosphere control.
表1Table 1
Figure PCTCN2020087699-appb-000001
Figure PCTCN2020087699-appb-000001
表2Table 2
Figure PCTCN2020087699-appb-000002
Figure PCTCN2020087699-appb-000002
评估烧结炉的性能时,标准差与CPK为主要指标。标准差是指所有尺寸波动的均匀性,值越小越好。CPK指衡量生产可行性指标,基准值为1.33,值越大越好。经过对比可知,采用双向气氛控制工艺后有效地改善了单向气氛控制工艺的不足。When evaluating the performance of a sintering furnace, the standard deviation and CPK are the main indicators. Standard deviation refers to the uniformity of fluctuations in all dimensions, and the smaller the value, the better. CPK refers to a measure of production feasibility, the benchmark value is 1.33, the larger the value, the better. The comparison shows that the use of the two-way atmosphere control process effectively improves the shortcomings of the one-way atmosphere control process.
本说明书中应用了具体个例对本发明的原理及实施方式进行了阐述,以上实施例的说明只是用于帮助理解本发明的方法及其核心思想;同时,对于本领域的一般技术人员,依据本发明的思想,在具体实施方式及应用范围上均会有改变之处。综上所述,本说明书内容不应理解为对本发明的限制。In this specification, specific examples are used to describe the principle and implementation of the present invention. The description of the above examples is only used to help understand the method and core idea of the present invention; at the same time, for those of ordinary skill in the art, according to this The idea of the invention will change in the specific implementation and the scope of application. In summary, the content of this specification should not be construed as a limitation to the present invention.

Claims (7)

  1. 一种双向气氛控制工艺,包括前期工序、烧结工序和后期工序,其特征在于,烧结工序中包括以下步骤:A two-way atmosphere control process, including a preliminary process, a sintering process, and a later process, characterized in that the sintering process includes the following steps:
    步骤A、向料箱内充入工艺气体,形成气体正向流动;Step A: Fill the material box with process gas to form a positive flow of gas;
    步骤B、向料箱内充入工艺气体,形成气体逆向流动。Step B: Fill the material box with process gas to form a reverse flow of gas.
  2. 根据权利要求1所述的双向气氛控制工艺,其特征在于,烧结工序中还包括以下步骤:The two-way atmosphere control process according to claim 1, wherein the sintering process further comprises the following steps:
    步骤C A、在料箱内抽真空,形成气体正向流动; Step C A , vacuum in the material box to form a positive flow of gas;
    步骤C B、在料箱内抽真空,形成气体逆向流动。 Step C B. Vacuum in the material box to form a reverse flow of gas.
  3. 一种双向气氛烧结炉,具有正向气氛控制结构,所述正向气氛控制结构包括正向进气结构和正向出气结构,气体由所述正向进气结构流入料箱内并由所述正向出气结构流出料箱,形成气体正向流动,其特征在于,还具有逆向气氛控制结构,所述逆向气氛控制结构具有逆向进气结构和逆向出气结构,气体由所述逆向进气结构流入并由所述逆向出气结构流出,形成气体逆向流动。A two-way atmosphere sintering furnace has a positive atmosphere control structure. The positive atmosphere control structure includes a forward gas inlet structure and a positive gas outlet structure. The material box flows out of the gas outlet structure to form a forward flow of gas. It is characterized in that it also has a reverse atmosphere control structure. The reverse atmosphere control structure has a reverse gas inlet structure and a reverse gas outlet structure. The gas flows out from the reverse air outlet structure to form a reverse flow of gas.
  4. 根据权利要求3所述的双向气氛烧结炉,其特征在于,所述正向进气结构为正向进气管,所述正向进气管的一端位于烧结炉外,所述正向进气管的另一端与烧结炉内的料箱连通,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;The two-way atmosphere sintering furnace according to claim 3, wherein the forward air inlet structure is a forward air inlet pipe, one end of the forward air inlet pipe is located outside the sintering furnace, and the other One end is in communication with the material box in the sintering furnace, the forward air outlet structure is a forward air outlet pipe, one end of the forward air outlet pipe is located outside the sintering furnace, and the other end of the forward air outlet pipe is connected to the material in the sintering furnace. Box connection
    所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,或所述逆向进气管与所述正向出气管均为独立管路且相邻设置,所述逆向出气结构为逆向出气管,所述逆向出气管为所述正向进气管的支管,或所述逆向出气管与所述正向进气管均为独立管路且相邻设置。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, or the reverse air intake pipe and the forward air outlet pipe are independent pipelines and are arranged adjacently, so The reverse air outlet structure is a reverse air outlet pipe, and the reverse air outlet pipe is a branch pipe of the forward air inlet pipe, or the reverse air outlet pipe and the forward air inlet pipe are independent pipelines and are arranged adjacently.
  5. 根据权利要求3所述的双向气氛烧结炉,其特征在于,所述正向进气结构为进气阀,所述进气阀固定于料箱上,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;The two-way atmosphere sintering furnace according to claim 3, wherein the positive air inlet structure is an air inlet valve, the air inlet valve is fixed on the material box, and the positive air outlet structure is a positive air outlet pipe , One end of the forward gas outlet pipe is located outside the sintering furnace, and the other end of the forward gas outlet pipe is in communication with the material box in the sintering furnace;
    所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,或所述逆向进气管与所述正向出气管均为独立管路且相邻设置,所述逆向出气结构为料箱上的拼接缝隙和门板缝隙。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, or the reverse air intake pipe and the forward air outlet pipe are independent pipelines and are arranged adjacently, so The reverse air outlet structure is the splicing gap on the material box and the door panel gap.
  6. 根据权利要求3所述的双向气氛烧结炉,其特征在于,所述正向进气结构为安全阀、料箱上的拼接缝隙、料箱上的门板缝隙,所述安全阀固定于料箱上,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;The two-way atmosphere sintering furnace according to claim 3, wherein the positive air intake structure is a safety valve, a splicing gap on the material box, and a door panel gap on the material box, and the safety valve is fixed on the material box , The positive gas outlet structure is a positive gas outlet pipe, one end of the positive gas outlet pipe is located outside the sintering furnace, and the other end of the positive gas outlet pipe is in communication with the material box in the sintering furnace;
    所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,或所述逆向进气管与所述正向出气管均为独立管路且相邻设置,所述逆向出气结构为料箱上的拼接缝隙和门板缝隙。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, or the reverse air intake pipe and the forward air outlet pipe are independent pipelines and are arranged adjacently, so The reverse air outlet structure is the splicing gap on the material box and the door panel gap.
  7. 根据权利要求3所述的双向气氛烧结炉,其特征在于,所述正向进气结构为料箱侧板上的开口,所述正向出气结构为正向出气管,所述正向出气管的一端位于烧结炉外,所述正向出气管的另一端与烧结炉内的料箱连通;The two-way atmosphere sintering furnace according to claim 3, wherein the positive air inlet structure is an opening on the side plate of the material box, the forward air outlet structure is a forward air outlet pipe, and the forward air outlet pipe One end of the sintering furnace is located outside the sintering furnace, and the other end of the forward gas outlet pipe is connected to the material box in the sintering furnace;
    所述逆向进气结构为逆向进气管,所述逆向进气管为所述正向出气管的支管,所述逆向出气结构为料箱侧板上的开口。The reverse air intake structure is a reverse air intake pipe, the reverse air intake pipe is a branch pipe of the forward air outlet pipe, and the reverse air outlet structure is an opening on a side plate of the material box.
PCT/CN2020/087699 2020-04-29 2020-04-29 Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace WO2021217474A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
PCT/CN2020/087699 WO2021217474A1 (en) 2020-04-29 2020-04-29 Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace
CN202080004093.9A CN112512728B (en) 2020-04-29 2020-04-29 Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace
JP2022600055U JP3241481U (en) 2020-04-29 2020-04-29 Two-way atmosphere sintering furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2020/087699 WO2021217474A1 (en) 2020-04-29 2020-04-29 Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace

Publications (1)

Publication Number Publication Date
WO2021217474A1 true WO2021217474A1 (en) 2021-11-04

Family

ID=74952810

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/087699 WO2021217474A1 (en) 2020-04-29 2020-04-29 Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace

Country Status (3)

Country Link
JP (1) JP3241481U (en)
CN (1) CN112512728B (en)
WO (1) WO2021217474A1 (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4859427A (en) * 1987-02-27 1989-08-22 Japan Atomic Energy Research Institute Active metal bed
JPH0747505B2 (en) * 1991-09-25 1995-05-24 日本碍子株式会社 Method of firing ceramic products
JP2011068947A (en) * 2009-09-25 2011-04-07 Jfe Steel Corp Method for cooling sintered ore and device therefor
CN203330401U (en) * 2013-06-27 2013-12-11 宁波恒普真空技术有限公司 Feed box interlayer air inflow device of metal powder injection molding vacuum degreasing sintering furnace
CN104180654A (en) * 2014-08-21 2014-12-03 重庆科技学院 Ultrasonic-vibration activation-assisted sintering tubular furnace
JP2018030102A (en) * 2016-08-25 2018-03-01 エヌ・イーケムキャット株式会社 Method for producing exhaust gas purifying catalyst
US20180073813A1 (en) * 2016-09-12 2018-03-15 Hamilton Sundstrand Corporation Counter-flow ceramic heat exchanger assembly and method
CN110603417A (en) * 2018-12-21 2019-12-20 宁波恒普真空技术有限公司 Vacuum degreasing sintering furnace and using method thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3052403B2 (en) * 1991-02-22 2000-06-12 株式会社村田製作所 Atmosphere firing furnace with batch type hearth rotation

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4859427A (en) * 1987-02-27 1989-08-22 Japan Atomic Energy Research Institute Active metal bed
JPH0747505B2 (en) * 1991-09-25 1995-05-24 日本碍子株式会社 Method of firing ceramic products
JP2011068947A (en) * 2009-09-25 2011-04-07 Jfe Steel Corp Method for cooling sintered ore and device therefor
CN203330401U (en) * 2013-06-27 2013-12-11 宁波恒普真空技术有限公司 Feed box interlayer air inflow device of metal powder injection molding vacuum degreasing sintering furnace
CN104180654A (en) * 2014-08-21 2014-12-03 重庆科技学院 Ultrasonic-vibration activation-assisted sintering tubular furnace
JP2018030102A (en) * 2016-08-25 2018-03-01 エヌ・イーケムキャット株式会社 Method for producing exhaust gas purifying catalyst
US20180073813A1 (en) * 2016-09-12 2018-03-15 Hamilton Sundstrand Corporation Counter-flow ceramic heat exchanger assembly and method
CN110603417A (en) * 2018-12-21 2019-12-20 宁波恒普真空技术有限公司 Vacuum degreasing sintering furnace and using method thereof

Also Published As

Publication number Publication date
CN112512728A (en) 2021-03-16
CN112512728B (en) 2023-02-10
JP3241481U (en) 2023-04-05

Similar Documents

Publication Publication Date Title
US9719727B2 (en) Fluid recirculation system for use in vapor phase particle production system
CN106975738A (en) Vacuum die-cast equipment and high vacuum die casting method
WO2021217474A1 (en) Bidirectional atmosphere control process and bidirectional atmosphere sintering furnace
CN207770759U (en) A kind of sand casting sand core combination structure and gas turbine cylinder
CN207848982U (en) A kind of ratio valve set system
CN206856026U (en) A kind of anticlogging 3D printer print head assembly
CN214842394U (en) Vacuum degreasing sintering system
CN104765385A (en) Electron beam selected area melting atmosphere adjust and control system and method
CN103331538B (en) A kind of copper pipe nitrogen charging and welding method and nitrogen charging welding controller
CN206190993U (en) Off -load formula pressure reducer
CN106086513B (en) A kind of electrovacuum copper molybdenum alloy and preparation method thereof
CN104034152A (en) High-temperature sintering equipment and sintering control method of nano carbonyl iron powder composite material
CN103882409B (en) The adjustable gas path device of source conveying ratio of mixture
CN108873953A (en) A kind of high-precision pressure control method and system based on electromagnetic proportional valve
CN107186217B (en) Tungsten powder reduction equipment and control method thereof
CN104494136B (en) A kind of dilatation mold
CN206011941U (en) The adjustable type cooling system of vacuum hotpressing machine
CN216801684U (en) Multidirectional atmosphere sintering furnace
CN104651946A (en) Silicon waveguide surface smoothing process based on silicon hydrogen bond current density method
CN207372286U (en) A kind of vacuum sintering furnace pumped vacuum systems
CN206677151U (en) Scroll plate is with vacuumizing mould
CN206475423U (en) A kind of blow moulding machine high-pressure gas circuit governor motion
CN102586988B (en) Production device and production process of hose line
CN206346888U (en) A kind of output control seat of air compressor machine
CN114192779A (en) Multidirectional atmosphere sintering furnace and multidirectional atmosphere control process

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20933798

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2022600055

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20933798

Country of ref document: EP

Kind code of ref document: A1